US10456742B2ActiveUtilityA1
Aqueous lime slurry, preparation process and uses
Est. expiryNov 19, 2032(~6.3 yrs left)· nominal 20-yr term from priority
B01D 2251/404B01D 53/502B01D 53/68B01D 53/64C01F 11/02B01D 53/1493B01F 3/0811B01D 53/48C02F 11/14B01F 23/4105C02F 11/148
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Claims
Abstract
Preparation of aqueous slurries of calcium dihydroxide. Preparation of aqueous suspensions of calcium hydroxide.
Claims
exact text as granted — not AI-modifiedThe invention claimed is:
1. An aqueous slurry of calcium hydroxide comprising water, calcium hydroxide, and a copolymer, said slurry having a dry content of at least 40% by weight, the viscosity of said aqueous slurry as measured by a Brookfield DVIII viscometer at 10 RPM being between 25 and 1,000 mPa·s at 20° C.,
wherein said copolymer consists:
of methacrylic acid monomers and/or any of its salts,
optionally of acrylic acid monomers and/or any of its salts,
of one or more monomers with the formula (I):
R—X—R′ (I)
where:
R represents a polymerizable unsaturated group,
R′ represents hydrogen or an alkyl group with from 1 to 4 carbon atoms,
X represents a structure with n unit(s) of ethylene oxide EO and m unit(s) of propylene oxide PO, arranged randomly or regularly, and
m and n are independent non-zero integers and are between 1 and 150, and wherein said slurry is prepared by a process comprising:
agitating a mixture of the water and the copolymer to form an aqueous solution;
adding the calcium hydroxide in powdered form to said aqueous solution and agitating to provide an initial slurry;
applying a homogeneous shear level greater than 50,000 s −1 to the initial slurry; and
optionally, while applying said shear level to said initial slurry, adding more copolymer and/or more powdered calcium hydroxide to said initial slurry.
2. The aqueous slurry according to claim 1 , wherein the copolymer has a molecular mass between 30,000 and 200,000 g/mol as determined by Gel Permeation Chromatography (GPC).
3. The aqueous slurry according to claim 1 , wherein the monomer of formula (I) is such that n+m>17.
4. The aqueous slurry according to claim 1 , wherein the R group of said monomer of formula (I) represents the methacrylate group.
5. The aqueous slurry according to claim 1 , wherein the R′ group of the monomer of formula (I) represents H or CH 3 .
6. The aqueous slurry according to claim 1 , wherein the monomer of formula (I) consists of, expressed as a percentage by weight of each of its components:
5 to 30% by weight of methacrylic acid monomers and/or any of its salts,
0 to 10% by weight of acrylic acid monomers and/or any of its salts,
70 to 95% by weight of monomers of formula (I).
7. The aqueous slurry according to claim 1 , wherein a mixer of the rotor-stator type is used to apply said shear.
8. The aqueous slurry according to claim 1 , wherein the shear is applied in a device equipped with a recirculating loop.
9. The aqueous slurry according to claim 1 , wherein the shear is applied in a device configured to deliver an output of at least 1,000 W/m 3 .
10. The aqueous slurry according to claim 1 , wherein the R group of said monomer of formula (I) represents an acrylate, methacrylate, methacrylurethane, vinyl or allyl group.
11. A method of treating industrial smoke, domestic wastewater, or industrial wastewater, comprising contacting said smoke or wastewater with the aqueous slurry according to claim 1 .
12. A method of flue gas desulfurization, comprising contacting industrial smoke with the aqueous slurry according to claim 1 .
13. A process for the preparation of the aqueous slurry of calcium hydroxide of claim 1 , the process comprising:
agitating a mixture of the water and the copolymer to form an aqueous solution;
adding the calcium hydroxide in powdered form to said aqueous solution and agitating to provide an initial slurry;
applying a homogeneous shear level greater than 50,000 s −1 to the initial slurry; and
optionally, while applying said shear level to said initial slurry, adding more copolymer and/or more powdered calcium hydroxide to said initial slurry.
14. A process according to claim 13 , wherein said process comprises adding more copolymer and/or more powdered calcium hydroxide to said initial slurry while applying said shear level to said initial slurry.Join the waitlist — get patent alerts
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